Compositions comprising metal-modified silica nanoparticles

ABSTRACT

A composition comprising particles with a transition metal imbedded therein is disclosed. Specifically, the mole ratio of transition metal to particles is from about 25:1 to about 50:1. The composition is prepared in the presence of ultrasonic energy. The particles are selected from the group consisting of organic particles, inorganic particles, and metal particles.

FIELD OF DISCLOSURE

The present disclosure relates generally to metal-modified silicaparticles and methods for preparing metal-modified silicanano-particles. More particularly, methods for ultrasonically mixing afirst and second formulation using an ultrasonic mixing system toprepare metal-modified silica particles are disclosed.

BACKGROUND OF DISCLOSURE

At least some known currently used odor control technologies areprepared by chemically depositing transition metal layers onto thesurface of silica nano-particles. For instance, U.S. Patent Pub. No,2005/0084438 to Do, et al., describes modifying the surface of silicaparticles with a transition metal so that the silica particles arebonded to the transition metal through a covalent or coordinate bond.Further, U.S. Patent Pub. No. 2006/0008442 to MacDonald, et al.describes modified nano-particles that have active sites that bindvarious gases and/or odorous compounds, thereby removing these compoundsfrom a medium such as air or water. The metal ions are absorbed onto thesurface of the nano-particle and bound strongly to the surface. Thesemodified nano-particles may be applied to nonwoven webs to provide odorremoving articles for industrial and consumer use. Although thesemodified nano-particles are useful, current procedures for forming thesenano-particles have multiple problems, which can waste time, energy, andmoney for manufacturers of these modified nano-particles.

Specifically, synthesis of this technology is sensitive to reagentconcentration, as aggregation and gelation in the reaction suspensionmay be observed at silica nano-particle concentrations above 4% (wt/wt).With this constraint, manufacturing and processing of the technology atthe production scale entails higher costs due to more energy expensed toremove higher volumes of solvent. Additionally, more substrate materialis needed in order to incorporate higher loading of technology into theproduct for increased odor removal efficacy. Particle agglomeration,also referred to herein as gelation, may be driven by a strong ionicstrength nature in the reaction media due to the chemicals in thatmedia.

Further, modified nano-particles formed by a stirred suspension ofsilica particles and copper salts with a base that is slowly addedresults in the active metal complex being formed on the surface of thesilica in discrete zones or nodes. It has been discovered that themodified nano-particles formed by this method are capable of converting,for example, thiols (mercaptans) odors into disulphides. The human noseis particularly sensitive to these odors and can detect the presence ofthiol odors down to part-per-billion (ppb). The human nose's ability todetect disulphides, however, is significantly less, in fact around tensof parts-per-million (ppm). Thus, the modified nano-particles mayconvert the malodor into a compound that can only be detected atsignificantly higher levels and therefore effectively converts the odorinto something the human nose cannot detect. The modified nano-particlescould perform this catalytic conversion continuously for an extendedperiod of time.

Once the modified nano-particles are formed, three major mechanisms areinvolved in remediation of odor compounds: (1) physical adsorption; (2)catalysis; and (3) chemical absorption. Physical adsorption is the mainpathway by which activated carbon material function. The advantages ofthis mechanism include rate and capacity effectiveness, however, theadsorption can be reversed at changes in temperature or humidity.Catalysis involves the conversion of an odor compound to anothercompound. Ideally, the converted compound should be heavier and posses ahigher boiling point and/or a lower vapor pressure, thus not allowing itto be re-emitted into the atmosphere. This is not guaranteed orpredictable, however, and may lead to disadvantages compared tosomething that is more irreversible. Chemical absorption involves thechemical binding of the odor compound to the odor removal compound.Typically, the binding is irreversible when subject to physicalchallenges such as temperature and humidity. It has been shown thatodorous compounds are removed from metal-modified silica nano-particlesvia the catalytic mechanism when the metal-modified silicanano-particles are prepared without the presence of ultrasound energy.

Based on the foregoing, there is a need in the art for a method ofpreparing metal-modified silica particles by ultrasonically mixing afirst and second formulation. Furthermore, it would be advantageous ifthe system could be configured to enhance the cavitation mechanism ofthe ultrasonics, thereby decreasing particle agglomeration and changingthe mechanism by which odorous compounds will be removed during use ofthe metal-modified particles.

SUMMARY OF DISCLOSURE

In one aspect, a method for preparing metal-modified particles byultrasonically mixing a first and second formulation comprises providinga treatment chamber comprising an elongate housing having longitudinallyopposite ends and an interior space. The housing is generally closed ata first longitudinal end and generally open at a second longitudinal endfor receiving a first and second formulation into the interior space ofthe housing, and at least one outlet port through which aparticulate-containing formulation is exhausted from the housingfollowing ultrasonic mixing of the first and second formulations. Theoutlet port is spaced longitudinally from the second longitudinal endsuch that liquid (i.e., first and/or second formulations) flowslongitudinally within the interior space of the housing from the secondlongitudinal end to the outlet port. In one embodiment, the housingincludes more than two separate ports for receiving additionalformulations to be mixed to prepare the metal-modified particles. Atleast one elongate ultrasonic waveguide assembly extends longitudinallywithin the interior space of the housing and is operable at apredetermined ultrasonic frequency to ultrasonically energize and mixthe first and second formulations (and any additional formulations)flowing within the housing.

The waveguide assembly generally comprises an elongate ultrasonic horndisposed at least in part intermediate the second longitudinal end andthe outlet port of the housing and has an outer surface located forcontact with the first and second formulations flowing within thehousing from the second longitudinal end to the outlet port. A pluralityof discrete agitating members are in contact with and extendtransversely outward from the outer surface of the horn intermediate thesecond longitudinal end and the outlet port in longitudinally spacedrelationship with each other. The agitating members and the horn areconstructed and arranged for dynamic motion of the agitating membersrelative to the horn upon ultrasonic vibration of the horn at thepredetermined frequency and to operate in an ultrasonic cavitation modeof the agitating members corresponding to the predetermined frequencyand the first and second formulations being mixed within the chamber.

As such, the present disclosure is directed to a method for preparingmetal-modified particles. The method comprises providing a treatmentchamber comprising an elongate housing having longitudinally oppositeends and an interior space, and an elongate ultrasonic waveguideassembly extending longitudinally within the interior space of thehousing and being operable at a predetermined ultrasonic frequency toultrasonically energize and mix a first and a second formulation flowingwithin the housing to prepare the metal-modified particles. The housingis closed at a first longitudinal end and open at a second longitudinalend for receiving a first and second formulation into the interior spaceof the housing, and at least one outlet port through which aparticulate-containing formulation is exhausted from the housingfollowing ultrasonic mixing of the first and second formulations. Theoutlet port is spaced longitudinally from the second longitudinal endsuch that the first and second formulations flow longitudinally withinthe interior space of the housing from the second longitudinal end tothe outlet port.

The waveguide assembly comprises an elongate ultrasonic horn disposed atleast in part intermediate the second longitudinal end and the outletport of the housing and having an outer surface located for contact withthe first and second formulations flowing within the housing from thesecond longitudinal end to the outlet port. Additionally, the waveguideassembly comprises a plurality of discrete agitating members in contactwith and extending transversely outward from the outer surface of thehorn intermediate the second longitudinal end and the outlet port inlongitudinally spaced relationship with each other. The agitatingmembers and the horn are constructed and arranged for dynamic motion ofthe agitating members relative to the horn upon ultrasonic vibration ofthe horn at the predetermined frequency and to operate in an ultrasoniccavitation mode of the agitating members corresponding to thepredetermined frequency and the first and second formulations beingmixed in the chamber.

The method further includes delivering the second formulation via thefirst inlet port into the interior space of the housing, delivering thesecond formulation via the second inlet port into the interior space ofthe housing, and ultrasonically mixing the first and second formulationsvia the elongate ultrasonic waveguide assembly operating in thepredetermined ultrasonic frequency.

The present invention is further directed to a method for preparingmetal-modified particles. The method comprises providing a treatmentchamber comprising an elongate housing having longitudinally oppositeends and an interior space, and an elongate ultrasonic waveguideassembly extending longitudinally within the interior space of thehousing and being operable at a predetermined ultrasonic frequency toultrasonically energize and mix a first and second formulation flowingwithin the housing. The housing is generally closed at least one of itslongitudinal ends and has at least a first inlet port for receiving thefirst formulation into the interior space of the housing, and a secondinlet port for receiving the second formulation into the interior spaceof the housing, and at least one outlet port through which aparticulate-containing formulation is exhausted from the housingfollowing ultrasonic mixing of the first and second formulations. Theoutlet port is spaced longitudinally from the first and second inletports such that the first and second formulations flow longitudinallywithin the interior space of the housing from the first and second inletports to the outlet port.

The waveguide assembly comprises an elongate ultrasonic horn disposed atleast in part intermediate the first and second inlet ports and theoutlet port of the housing and having an outer surface located forcontact with the first and second formulations flowing within thehousing from the first and second inlet ports to the outlet port; aplurality of discrete agitating members in contact with and extendingtransversely outward from the outer surface of the horn intermediate thefirst and second inlet ports and the outlet port in longitudinallyspaced relationship with each other; and a baffle assembly disposedwithin the interior space of the housing and extending at least in parttransversely inward from the housing toward the horn to directlongitudinally flowing first and second formulations in the housing toflow transversely inward into contact with the agitating members. Theagitating members and the horn are constructed and arranged for dynamicmotion of the agitating members relative to the horn upon ultrasonicvibration of the horn at the predetermined frequency and to operate inan ultrasonic cavitation mode of the agitating members corresponding tothe predetermined frequency and the first and second formulations beingmixed in the chamber.

The method further comprises delivering the first formulation via thefirst inlet port into the interior space of the housing, delivering thesecond formulation via the second inlet port into the interior space ofthe housing, and ultrasonically mixing the first and second formulationsvia the elongate ultrasonic waveguide assembly operating in thepredetermined ultrasonic frequency.

The present disclosure is further directed to a method for reducing odorusing an ultrasonic mixing system as is described above. The methodcomprises preparing metal-modified silica particles, isolating themetal-modified silica particles, and contacting the metal modifiedsilica particles to an odorous compound.

Other features of the present disclosure will be in part apparent and inpart pointed out hereinafter.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a schematic of an ultrasonic mixing system according to afirst embodiment of the present disclosure for preparing metal-modifiedsilica particles.

FIG. 2 is a schematic of an ultrasonic mixing system according to asecond embodiment of the present disclosure for preparing metal-modifiedsilica particles.

FIG. 3 is a schematic of an ultrasonic mixing system according to athird embodiment of the present disclosure for preparing metal-modifiedsilica particles.

FIG. 4 depicts a graph showing ethyl mercaptan removal over time asdescribed in Example 1.

FIG. 5 depicts a graph showing remediation of ethyl mercaptan over timeas described in Example 5.

FIG. 6 depicts a graph showing headspace gas chromatograms for theremediation of ethyl mercaptan (EtSH).

FIG. 7A depicts mass spectroscopy (MS) chromatograms from GC/MSexperiments for the GC peak at approximately 3.5 minutes (r.t.).

FIG. 7B depicts mass spectroscopy (MS) chromatograms from GC/MSexperiments for the GC peak at approximately 13.5 minutes (r.t.).

FIG. 8A depicts EPR spectra for copper modified silica particles fromExample 2.

FIG. 8B depicts EPR spectra for copper modified silica particles fromExample 3.

FIG. 9A depicts XPS spectra for copper modified silica particles fromExample 2.

FIG. 9B depicts XPS spectra for copper modified silica particles fromExample 3.

FIG. 10 depicts BJH pore size analyses for copper modified silicaparticles.

Corresponding reference characters indicate corresponding partsthroughout the drawings.

DETAILED DESCRIPTION

With particular reference now to FIG. 1, in one embodiment, anultrasonic mixing system, generally indicated at 121, for mixing a firstand second formulation to prepare metal-modified particles generallycomprises a treatment chamber, indicated at 151, that is operable toultrasonically mix various formulations to form metal-modifiedparticles, and further is capable of creating a cavitation mode thatallows for better mixing within the housing of the chamber 151. Byultrasonically mixing the first and second formulations, agglomerationof the silica nano-particles can be significantly reduced, and themechanism by which metal-modified silica particles remove odorouscompounds is changed.

More specifically, by exposing the first and second formulations toultrasonic energy, a number of factors take advantage of the uniquesonochemistry and cavitation activities occurring within the mixtureduring passage through the chamber that is being mixed by the baffles.While the elemental composition of the metal-modified silica particlesis the same as a solution deposition system, it differs in numerousphysical and performance characteristics. First, with regard to physicalcharacteristics, the metal is not merely deposited on the surface of thesilica particle but rather is imbedded below the subsurface of theparticle. Analytically, no trace of the metal can be detected on thesurface. Further, the surface area of the particles is higher than thatof a solution deposition method system. This is due to smallpothole-like holes etched into the surface of the silica particles. Inaddition, with regard to performance characteristics, the metal speciesdoes not have catalytic functionality, but rather, has straightabsorption of malodor compounds. Thus, this composition absorbs thiol(mercaptan) odor molecules and locks them into a complex. Although thiscomposition does eventually reach a saturation point, which is incontrast to the solution deposition composition, these metal-modifiedparticles are still a very effective odor/malodor absorbent. As such, itcan be concluded that a different type of metal complex species has beengenerated using method of preparation inclusive of the presence ofultrasonic energy.

While not fully understood, it is believed that in the ultrasonicchamber, the metal ions are forcefully imbedded into the sub-surface ofthe nano-particles by the extraordinary forces involved in thecavitation process. The localized high temperatures and pressures mayalso contribute to the new metal complex formed therein.

It is generally believed that as ultrasonic energy is created by thewaveguide assembly, increased cavitation of the formulations occurs,creating microbubbles. As these microbubbles then collapse, the pressurewithin the chamber is increased forcibly dispersing the particles of thesecond formulation within and throughout the first and secondformulations.

More specifically, ultrasonic cavitation is a process by which extremepressures, temperatures, and velocities can be generated on a very smallscale for very short periods of time. The mechanism producing theseconditions is the nucleation, growth, and violent collapse of cavitation“bubbles”. These bubbles are formed in several ways when mechanicalpressure waves (alternating compression and rarefaction) are introducedinto a fluid. During the rarefaction phase of the pressure wave, theliquid molecules are pulled against the liquid's natural elastic andmolecular bonding forces. With sufficient intensity, the negativepressure can exceed the tensile strength of the liquid and generate avacuum nucleus in the liquid. The voids typically form first at natural“weak” points in the liquid such as entrained gas in the pores ofsuspended particulates or small remnant bubbles from previous cavitationevents, however, these are not a requirement. During the compressionphase of the wave, the void collapses.

Once a bubble is formed, if the expansion phase is fast enough, thebubble will not be able to fully collapse and it will continue to growuntil it reaches a size described as the resonant point (in water, 170microns at 20 kHz). At this size, the bubble can efficiently absorb theultrasound energy, and the bubble grows rapidly until it reaches a sizewhere the efficient absorption diminishes and the bubble violentlycollapses.

Another means by which bubble growth occurs at a slower pace isdescribed as “rectified diffusion”. A small gas bubble grows during therarefaction phase of the mechanical pressure wave and gas begins todiffuse into the bubble from the liquid. As the bubble begins to shrinkduring the compression phase of the mechanical pressure wave, gas beginsto diffuse out of the bubble back into the liquid. The rate of diffusionis directly related to the surface area of the bubble. On average, thebubble surface area is smaller during the compression phase than it isduring the expansion phase. Therefore, more gas diffuses into the bubblethan can diffuse out so the oscillating bubble grows. Once a criticalsize is reached, the process can no longer sustain itself and the bubblecollapses.

In either situation, the violent collapse results in the rapid (muchless than a microsecond) compression of the gas to a pressure of about1,000 atmospheres resulting in a temperature increase of about 5000° C.The shock waves produced by the numerous cavitation events result inextremely turbulent micro-mixing and high-speed particle collisions.These inter-particle collisions have been shown to be sufficientlyenergetic to melt together metal particles at transient temperaturesdetermined to be up to about 3000° C. at the point of collision. Theinter-particle collisions can also have a dramatic effect on particlemorphology remarkably changing the size, surface, and composition ofparticles.

When a cavitation bubble is formed and collapses near a surface, anotherphenomenon is observed. Due to the non-homogeneous boundary conditions,the bubble implodes asymmetrically and generates a very small,high-velocity (measured at about 400 km/hr) jet of liquid toward thesurface. This energetic jet can cause severe damage to surfaces and isthe effect responsible for the cavitation erosion that is observedduring ultrasonic liquid processing, as well as any high-speed fluidflow event that results in cavitation (e.g., liquid pumping, shippropellers).

When a cavitation bubble is formed and collapses away from a surface, itdoes so symmetrically (spherically). A surface must be several timeslarger than the bubble to generate asymmetrical bubble collapse.Therefore, fine particle dispersions will not produce the liquid jettingeffect.

The ultrasonic cavitation effect is influenced by the frequency andintensity of the mechanical pressure waves generated within the liquidas well as the properties of the liquid itself. The number of cavitationsites is known to be directly proportional to the excitation frequency,however, the average size of the cavitation bubble is inverselyproportional to the frequency. In water at 20 kHz, the cavitationthreshold intensity has been empirically determined to be 0.3 W/cm².Liquid properties that influence cavitation include vapor pressure,temperature, density, viscosity, and surface tension.

The ultrasonic treatment device described herein has an advantage overmost other known devices in that it can achieve acoustic intensitiesseveral (3 or more) orders of magnitude above the cavitation thresholdlevel and significantly higher than other commercial systems.

The terms “liquid” and “formulation” are used interchangeably to referto a single component formulation, a formulation comprised of two ormore components in which at least one of the components is a liquid suchas a liquid-liquid formulation, a liquid-gas formulation, or aliquid-solid formulation.

The ultrasonic mixing system 121 is illustrated schematically in FIG. 1and further described herein with reference to use of the treatmentchamber 151 in the ultrasonic mixing system to mix various formulationsto create metal-modified particles. The metal-modified particles cansubsequently be used to remove odorous compounds from a medium such asair or water. For example, in one embodiment, a first formulationcomprising aqueous sodium bicarbonate is ultrasonically mixed with asecond formulation comprising silica nano-particles and a copper (II)salt aqueous formulation to form copper-modified silica nano-particlesfor use in removing odorous compounds. It should be understood by oneskilled in the art that while described herein with respect to a firstformulation comprising aqueous sodium bicarbonate and a secondformulation comprising silica nano-particles and a chloride salt ofcopper(II) aqueous formulation, the first formulation may comprise anybasic buffer system and the second formulation may comprise silicanano-particles with a chloride salt of any transition metal.

Specifically, the first formulation may comprise any basic buffer systemcapable of maintaining the pH of the first formulation from about 8 toabout 10. For instance, the basic buffer system may include potassiumhydroxide, sodium hydroxide, ammonium hydroxide, sodium carbonate, andcombinations thereof. Without intending to be limited by theory, it isbelieved that the purpose of the base in the buffer system is todeprotonate the silanol groups on the silica surface, which allows thetransition metal to chemically form a bond with the deprotonatedsilanol.

Further, the silica nano-particles included within the secondformulation may possess various forms, shapes, and sizes depending uponthe desired result. For instance, the silica particles may be in theshape of a sphere, crystal, rod, disk, tube, string, and the like. Theaverage size of the silica particles is generally less than about 500microns, in some embodiments less than about 100 microns, in someembodiments less than about 100 nanometers, in some embodiments fromabout 1 to about 50 nanometers, in some embodiments from about 2 toabout 50 nanometers, and in some embodiments, from about 4 to about 20nanometers. As used herein, the average size of a particle refers to itsaverage length, width, height, and/or diameter.

The silica particles may have a surface area of from about 50 squaremeters per gram (m²/g) to about 1000 m²/g, in some embodiments fromabout 100 m²/g to about 600 m²/g, and in some embodiments, from about180 m²/g to about 240 m²/g. Surface area may be determined by thephysical gas adsorption (B.E.T.) method of Brunauer, Emmet, and Teller,Journal of American Chemical Society, Vol. 60, 1938, p. 309, withnitrogen as the adsorption gas. If desired, the silica particles mayalso be relatively nonporous or solid. That is, the silica particles mayhave a pore volume that is less than about 0.5 milliliters per gram(ml/g), in some embodiments less than about 0.4 milliliters per gram, insome embodiments less than about 0.3 ml/g, and in some embodiments, fromabout 0.2 ml/g to about 0.3 ml/g. Without intending to be limited bytheory, it is believed that silica particles having such small size andhigh surface area may improve the adsorption capability of the silicafor many odorous compounds. Moreover, it is believed that the solidnature, i.e., low pore volume, of the silica particles may enhance theuniformity and stability of the silica, without sacrificing its odoradsorption characteristics. Commercially available examples of silicanano-particles, such as described above, include Snowtex®-C, Snowtex®-O,Snowtex®-PS, and Snowtex®-OXS, which are available from Nissan ChemicalAmerica Corporation of Houston, Tex. Snowtex-OXS particles, forinstance, have a particle size of from 4 to 6 nanometers, and may beground into a powder having a surface area of approximately 509 squaremeters per gram.

The concentration of silica particles in the second formulation is fromabout 0.01% to about 10% (by weight) in water. In one embodiment, theconcentration of silica particles in the second formulation is at leastabout 4% (by weight) in water. In another embodiment, the concentrationof silica particles in the second formulation is about 5% (by weight) inwater.

Although described herein with respect to silica, other materials may beused in accordance with the present disclosure to form metal modifiedparticles. For instance, the particles could be selected from inorganicmaterials, such as silica, alumina, or zeolite; metals, such as silver,copper, or gold; organic materials, such as polystyrene, latex,polyethylene glycol, or a lipid micelle; or a microbe including a lipidor saccharide-based wall. Further, the present disclosure may be used inpreparing metal-modified flat surfaces comprised of metal, organicfilms, inorganic films, sheets, or fibers.

In addition, the second formulation may comprise silica nano-particleswith a salt of any transition metal. Examples of suitable transitionmetals that may be used in the methods of the present disclosure,include, but are not limited to, scandium, titanium, vanadium, chromium,manganese, iron, cobalt, nickel, copper, zinc, silver, and gold. Thesecond formulation may comprise silica nano-particles with chloridesalts of Cu(II), Fe(II), Mn(II), and Co(II). Without being limited bytheory, it is believed that the transition metal provides one or moreactive sites for capturing and/or neutralizing an odorous compound.Further, the presence of the transition metal is also believed to helpimprove the Lewis acidity of the silica, thus rendering it morereceptive to free electron pairs of many odorous compounds. In addition,the point of contact for chemical absorption of the odor compound to themetal-modified silica particle is the metal site. In an alternativeembodiment, other materials may also be used in the second formulationin accordance with the present disclosure. These other materials mayinclude metals; organic molecules, such as dyes, pharmaceuticals,antimicrobials, UV absorbing molecules, and the like; enzymes,biomolecules; and microbes, such as bacteria, molds, viruses, andspores. These embedded species may be used for ease of handling, use,and removal, and could also be used as triggerable controlled releasesystems which could release these embedded species when needed.

The transition metal is present in the second formulation from about 13%to about 40% by weight of the second formulation. The mole ratio of thetransition metal to the silica particles present in the secondformulation may be selectively varied to achieve the desired results. Inmost embodiments, for example, the mole ratio of transition metal to thesilica particles is at least about 5:1, in some embodiments at leastabout 50:1, and in some embodiments, at least about 200:1. In apreferred embodiment, the second formulation comprises silica particlesdispersed in a chloride salt of copper(II) aqueous formulation in a moleratio of chloride salt of copper(II) to silica particles of about 50:1.

In one particularly preferred embodiment, as illustrated in FIG. 1, thetreatment chamber 151 is generally elongate and has a general inlet end125 (an upper end in the orientation of the illustrated embodiment) anda general outlet end 127 (a lower end in the orientation of theillustrated embodiment). The treatment chamber 151 is configured suchthat the first formulation enters the treatment chamber 151 generally atthe inlet end 125 thereof, flows generally longitudinally within thechamber (e.g., downward in the orientation of illustrated embodiment)and exits the chamber generally at the outlet end 127 of the chamber.

The terms “upper” and “lower” are used herein in accordance with thevertical orientation of the treatment chamber 151 illustrated in thevarious drawings and are not intended to describe a necessaryorientation of the chamber in use. That is, while the chamber 151 ismost suitably oriented vertically, with the outlet end 127 of thechamber below the inlet end 125 as illustrated in the drawing, it shouldbe understood that the chamber may be oriented with the inlet end belowthe outlet end and the first and second formulations are mixed as thefirst formulation travels upward through the chamber, or it may beoriented other than in a vertical orientation and remain within thescope of this disclosure.

The terms “axial” and “longitudinal” refer directionally herein to thevertical direction of the chamber 151 (e.g., end-to-end such as thevertical direction in the illustrated embodiment of FIG. 1). The terms“transverse”, “lateral” and “radial” refer herein to a direction normalto the axial (e.g., longitudinal) direction. The terms “inner” and“outer” are also used in reference to a direction transverse to theaxial direction of the treatment chamber 151, with the term “inner”referring to a direction toward the interior of the chamber and the term“outer” referring to a direction toward the exterior of the chamber.

The inlet end 125 of the treatment chamber 151 is in fluid communicationwith a suitable delivery system, generally indicated at 129, that isoperable to direct one formulation to, and more suitably through, thechamber 151. Typically, the delivery system 129 may comprise one or morepumps 171 operable to pump the respective formulation from acorresponding source thereof to the inlet end 125 of the chamber 151 viasuitable conduits 134.

It is understood that the delivery system 129 may be configured todeliver more than one formulation to the treatment chamber 151 withoutdeparting from the scope of this disclosure. It is also contemplatedthat delivery systems other than that illustrated in FIG. 1 anddescribed herein may be used to deliver one or more formulations to theinlet end 125 of the treatment chamber 151 without departing from thescope of this disclosure. It should be understood that more than oneformulation can refer to two streams of the same formulation ordifferent formulations being delivered to the inlet end of the treatmentchamber without departing from the scope of the present disclosure.

The treatment chamber 151 comprises a housing defining an interior space153 of the chamber 151 through which the first formulation delivered tothe chamber 151 flows from the inlet end 125 to the outlet end 127thereof after the second formulation has been added to the chamber 151.The chamber housing 151 suitably comprises an elongate tube 155generally defining, at least in part, a sidewall 157 of the chamber 151.It should be understood by one skilled in the art that the inlet end ofthe housing may include one or more inlet ports, two or more inletports, and even three or more inlet ports. For example, FIG. 3, asdiscussed in more detail below, illustrates an embodiment comprising aninlet port for delivering the first formulation to the chamber and aseparate inlet port for delivering the second formulation to thechamber. Alternatively, although not shown, the housing may comprisethree inlet ports, wherein the first inlet port and the second inletport are suitable in parallel, spaced relationship with each other, andthe third inlet port is oriented on the opposite sidewall of the housingfrom the first and second inlet ports. Further, it should be understoodby one skilled in the art that an open longitudinal end of the elongatetube 155 may be used as an inlet or an outlet port.

As shown in FIG. 1, the inlet end 125 is generally open to thesurrounding environment. In an alternative embodiment (not shown),however, the housing may comprise a closure connected to andsubstantially closing the longitudinally opposite end of the sidewall,and having at least one inlet port therein to generally define the inletend of the treatment chamber. The sidewall (e.g., defined by theelongate tube) of the chamber has an inner surface that together withthe waveguide assembly (as described below) and the closure define theinterior space of the chamber.

In the illustrated embodiment of FIG. 1, the tube 155 is generallycylindrical so that the chamber sidewall 157 is generally annular incross-section. However, it is contemplated that the cross-section of thechamber sidewall 157 may be other than annular, such as polygonal oranother suitable shape, and remains within the scope of this disclosure.The chamber sidewall 157 of the illustrated chamber 151 is suitablyconstructed of a transparent material, although it is understood thatany suitable material may be used as long as the material is compatiblewith the formulations and particulates being mixed within the chamber,the pressure at which the chamber is intended to operate, and otherenvironmental conditions within the chamber such as temperature.

A waveguide assembly, generally indicated at 203, extends longitudinallyat least in part within the interior space 153 of the chamber 151 toultrasonically energize the formulation (and any of its components)flowing through the interior space 153 of the chamber 151. Inparticular, the waveguide assembly 203 of the illustrated embodimentextends longitudinally from the lower or outlet end 127 of the chamber151 up into the interior space 153 thereof to a terminal end 113 of thewaveguide assembly disposed intermediate the inlet end 125. Althoughillustrated in FIG. 1 as extending longitudinally into the interiorspace 153 of the chamber 151, it should be understood by one skilled inthe art that the waveguide assembly may extend laterally from a housingsidewall of the chamber, running horizontally through the interior spacethereof without departing from the scope of the present disclosure.Typically, the waveguide assembly 203 is mounted, either directly orindirectly, to the chamber housing 151 as will be described laterherein.

Still referring to FIG. 1, the waveguide assembly 203 suitably comprisesan elongate horn assembly, generally indicated at 133, disposed entirelywith the interior space 153 of the housing 151 intermediate the inletend 125 and the outlet port 165 for complete submersion within theliquid being treated within the chamber 151, and more suitably, in theillustrated embodiment, it is aligned coaxially with the chambersidewall 157. The horn assembly 133 has an outer surface 107 thattogether with an inner surface 167 of the sidewall 157 defines a flowpath within the interior space 153 of the chamber 151 along which theformulation (and its components) flow past the horn within the chamber(this portion of the flow path being broadly referred to herein as theultrasonic treatment zone). The horn assembly 133 has an upper enddefining a terminal end of the horn assembly (and therefore the terminalend 113 of the waveguide assembly) and a longitudinally opposite lowerend 111. Although not shown, it is particularly preferable that thewaveguide assembly 203 also comprises a booster coaxially aligned withand connected at an upper end thereof to the lower end 111 of the hornassembly 133. It is understood, however, that the waveguide assembly 203may comprise only the horn assembly 133 and remain within the scope ofthis disclosure. It is also contemplated that the booster may bedisposed entirely exterior of the chamber housing 151, with the hornassembly 133 mounted on the chamber housing 151 without departing fromthe scope of this disclosure.

The waveguide assembly 203, and more particularly the booster issuitably mounted on the chamber housing 151, e.g., on the tube 155defining the chamber sidewall 157, at the upper end thereof by amounting member (not shown) that is configured to vibrationally isolatethe waveguide assembly (which vibrates ultrasonically during operationthereof) from the treatment chamber housing. That is, the mountingmember inhibits the transfer of longitudinal and transverse mechanicalvibration of the waveguide assembly 203 to the chamber housing 151 whilemaintaining the desired transverse position of the waveguide assembly(and in particular the horn assembly 133) within the interior space 153of the chamber housing and allowing both longitudinal and transversedisplacement of the horn assembly within the chamber housing. Themounting member also at least in part (e.g., along with the booster,lower end of the horn assembly) closes the outlet end 127 of the chamber151. Examples of suitable mounting member configurations are illustratedand described in U.S. Pat. No. 6,676,003, the entire disclosure of whichis incorporated herein by reference to the extent it is consistentherewith.

In one particularly suitable embodiment, the mounting member is ofsingle piece construction. Even more suitably the mounting member may beformed integrally with the booster (and more broadly with the waveguideassembly 203). However, it is understood that the mounting member may beconstructed separately from the waveguide assembly 203 and remain withinthe scope of this disclosure. It is also understood that one or morecomponents of the mounting member may be separately constructed andsuitably connected or otherwise assembled together.

In one suitable embodiment, the mounting member is further constructedto be generally rigid (e.g., resistant to static displacement underload) so as to hold the waveguide assembly 203 in proper alignmentwithin the interior space 153 of the chamber 151. For example, the rigidmounting member in one embodiment may be constructed of anon-elastomeric material, more suitably metal, and even more suitablythe same metal from which the booster (and more broadly the waveguideassembly 203) is constructed. The term “rigid” is not, however, intendedto mean that the mounting member is incapable of dynamic flexing and/orbending in response to ultrasonic vibration of the waveguide assembly203. In other embodiments, the rigid mounting member may be constructedof an elastomeric material that is sufficiently resistant to staticdisplacement under load but is otherwise capable of dynamic flexingand/or bending in response to ultrasonic vibration of the waveguideassembly 203.

A suitable ultrasonic drive system 131 including at least an exciter(not shown) and a power source (not shown) is disposed exterior of thechamber 151 and operatively connected to the booster (not shown) (andmore broadly to the waveguide assembly 203) to energize the waveguideassembly to mechanically vibrate ultrasonically. Examples of suitableultrasonic drive systems 131 include a Model 20A3000 system availablefrom Dukane Ultrasonics of St. Charles, Ill., and a Model 2000CS systemavailable from Herrmann Ultrasonics of Schaumberg, Ill.

In one embodiment, the drive system 131 is capable of operating thewaveguide assembly 203 at a frequency in the range of about 15 kHz toabout 100 kHz, more suitably in the range of about 15 kHz to about 60kHz, and even more suitably in the range of about 20 kHz to about 40kHz. Such ultrasonic drive systems 131 are well known to those skilledin the art and need not be further described herein.

In some embodiments, however not illustrated, the treatment chamber caninclude more than one waveguide assembly having at least two hornassemblies for ultrasonically treating and mixing the phases together toprepare the emulsion. As noted above, the treatment chamber comprises ahousing defining an interior space of the chamber through which theformulations are delivered from an inlet end. The housing comprises anelongate tube defining, at least in part, a sidewall of the chamber. Aswith the embodiment including only one waveguide assembly as describedabove, the tube may have one or more inlet ports formed therein, throughwhich at least two formulations to be mixed within the chamber aredelivered to the interior space thereof, and at least one outlet portthrough which the particulate-containing formulation exits the chamber.

In such an embodiment, two or more waveguide assemblies extendlongitudinally at least in part within the interior space of the chamberto ultrasonically energize and mix the formulations (and resultingparticulate containing formulation) flowing through the interior spaceof the chamber. Each waveguide assembly separately includes an elongatehorn assembly, each disposed entirely within the interior space of thehousing intermediate the inlet end 125 and the outlet port for completesubmersion within the formulations being mixed within the chamber. Eachhorn assembly can be independently constructed as described more fullyherein (including the horns, along with the plurality of agitatingmembers and baffle assemblies).

Referring back to FIG. 1, the horn assembly 133 comprises an elongate,generally cylindrical horn 105 having an outer surface 107, and two ormore (i.e., a plurality of) agitating members 137 connected to the hornand extending at least in part transversely outward from the outersurface of the horn in longitudinally spaced relationship with eachother. The horn 105 is suitably sized to have a length equal to aboutone-half of the resonating wavelength (otherwise commonly referred to asone-half wavelength) of the horn. In one particular embodiment, the horn105 is suitably configured to resonate in the ultrasonic frequencyranges recited previously, and most suitably at 20 kHz. For example, thehorn 105 may be suitably constructed of a titanium alloy (e.g., Ti₆Al₄V)and sized to resonate at 20 kHz. The one-half wavelength horn 105operating at such frequencies thus has a length (corresponding to aone-half wavelength) in the range of about 4 inches to about 6 inches,more suitably in the range of about 4.5 inches to about 5.5 inches, evenmore suitably in the range of about 5.0 inches to about 5.5 inches, andmost suitably a length of about 5.25 inches (133.4 mm). It isunderstood, however, that the treatment chamber 151 may include a horn105 sized to have any increment of one-half wavelength without departingfrom the scope of this disclosure.

In one embodiment (not shown), the agitating members 137 comprise aseries of five washer-shaped rings that extend continuously about thecircumference of the horn in longitudinally spaced relationship witheach other and transversely outward from the outer surface of the horn.In this manner the vibrational displacement of each of the agitatingmembers relative to the horn is relatively uniform about thecircumference of the horn. It is understood, however, that the agitatingmembers need not each be continuous about the circumference of the horn.For example, the agitating members may instead be in the form of spokes,blades, fins or other discrete structural members that extendtransversely outward from the outer surface of the horn. For example, asillustrated in FIG. 1, one of the five agitating members is in a T-shape701. Specifically, the T-shaped agitating member 701 surrounds the nodalregion. It has been found that members in the T-shape, generate a strongradial (e.g., horizontal) acoustic wave that further increases thecavitation effect as described more fully herein.

By way of a dimensional example, the horn assembly 133 of theillustrated embodiment of FIG. 1 has a length of about 5.25 inches(133.4 mm), one of the rings 137 is suitably disposed adjacent theterminal end 113 of the horn 105 (and hence of the waveguide assembly203), and more suitably is longitudinally spaced approximately 0.063inches (1.6 mm) from the terminal end of the horn 105. In otherembodiments the uppermost ring may be disposed at the terminal end ofthe horn 105 and remain within the scope of this disclosure. The rings137 are each about 0.125 inches (3.2 mm) in thickness and arelongitudinally spaced from each other (between facing surfaces of therings) a distance of about 0.875 inches (22.2 mm).

It is understood that the number of agitating members 137 (e.g., therings in the illustrated embodiment) may be less than or more than fivewithout departing from the scope of this disclosure. It is alsounderstood that the longitudinal spacing between the agitating members137 may be other than as illustrated in FIG. 1 and described above(e.g., either closer or spaced further apart). Furthermore, while therings 137 illustrated in FIG. 1 are equally longitudinally spaced fromeach other, it is alternatively contemplated that where more than twoagitating members are present the spacing between longitudinallyconsecutive agitating members need not be uniform to remain within thescope of this disclosure.

In particular, the locations of the agitating members 137 are at leastin part a function of the intended vibratory displacement of theagitating members upon vibration of the horn assembly 133. For example,in the illustrated embodiment of FIG. 1, the horn assembly 133 has anodal region located generally longitudinally centrally of the horn 105(e.g., at the third ring). As used herein and more particularly shown inFIG. 1, the “nodal region” of the horn 105 refers to a longitudinalregion or segment of the horn member along which little (or no)longitudinal displacement occurs during ultrasonic vibration of the hornand transverse (e.g., radial in the illustrated embodiment) displacementof the horn is generally maximized. Transverse displacement of the hornassembly 133 suitably comprises transverse expansion of the horn but mayalso include transverse movement (e.g., bending) of the horn.

In the illustrated embodiment of FIG. 1, the configuration of theone-half wavelength horn 105 is such that the nodal region isparticularly defined by a nodal plane (i.e., a plane transverse to thehorn member at which no longitudinal displacement occurs whiletransverse displacement is generally maximized) is present. This planeis also sometimes referred to as a “nodal point”. Accordingly, agitatingmembers 137 (e.g., in the illustrated embodiment, the rings) that aredisposed longitudinally further from the nodal region of the horn 105will experience primarily longitudinal displacement while agitatingmembers that are longitudinally nearer to the nodal region willexperience an increased amount of transverse displacement and adecreased amount of longitudinal displacement relative to thelongitudinally distal agitating members.

It is understood that the horn 105 may be configured so that the nodalregion is other than centrally located longitudinally on the horn memberwithout departing from the scope of this disclosure. It is alsounderstood that one or more of the agitating members 137 may belongitudinally located on the horn so as to experience both longitudinaland transverse displacement relative to the horn upon ultrasonicvibration of the horn 105.

Still referring to FIG. 1, the agitating members 137 are sufficientlyconstructed (e.g., in material and/or dimension such as thickness andtransverse length, which is the distance that the agitating memberextends transversely outward from the outer surface 107 of the horn 105)to facilitate dynamic motion, and in particular dynamic flexing/bendingof the agitating members in response to the ultrasonic vibration of thehorn. In one particularly suitable embodiment, for a given ultrasonicfrequency at which the waveguide assembly 203 is to be operated in thetreatment chamber (otherwise referred to herein as the predeterminedfrequency of the waveguide assembly) and a particular liquid to betreated within the chamber 151, the agitating members 137 and horn 105are suitably constructed and arranged to operate the agitating membersin what is referred to herein as an ultrasonic cavitation mode at thepredetermined frequency.

As used herein, the ultrasonic cavitation mode of the agitating membersrefers to the vibrational displacement of the agitating memberssufficient to result in cavitation (i.e., the formation, growth, andimplosive collapse of bubbles in a liquid) of the formulation beingprepared at the predetermined ultrasonic frequency. For example, wherethe formulations (and particulates) flowing within the chamber compriseaqueous liquid formulations, and the ultrasonic frequency at which thewaveguide assembly 203 is to be operated (i.e., the predeterminedfrequency) is about 20 kHZ, one or more of the agitating members 137 aresuitably constructed to provide a vibrational displacement of at least1.75 mils (i.e., 0.00175 inches, or 0.044 mm) to establish a cavitationmode of the agitating members.

It is understood that the waveguide assembly 203 may be configureddifferently (e.g., in material, size, etc.) to achieve a desiredcavitation mode associated with the particular formulation and/orparticulates to be mixed. For example, as the viscosity of theformulation being mixed with the particulates changes, the cavitationmode of the agitating members may need to be changed.

In particularly suitable embodiments, the cavitation mode of theagitating members corresponds to a resonant mode of the agitatingmembers whereby vibrational displacement of the agitating members isamplified relative to the displacement of the horn. However, it isunderstood that cavitation may occur without the agitating membersoperating in their resonant mode, or even at a vibrational displacementthat is greater than the displacement of the horn, without departingfrom the scope of this disclosure.

In one suitable embodiment, a ratio of the transverse length of at leastone and, more suitably, all of the agitating members to the thickness ofthe agitating member is in the range of about 2:1 to about 6:1. Asanother example, the rings each extend transversely outward from theouter surface 107 of the horn 105 a length of about 0.5 inches (12.7 mm)and the thickness of each ring is about 0.125 inches (3.2 mm), so thatthe ratio of transverse length to thickness of each ring is about 4:1.It is understood, however that the thickness and/or the transverselength of the agitating members may be other than that of the rings asdescribed above without departing from the scope of this disclosure.Also, while the agitating members 137 (rings) may suitably each have thesame transverse length and thickness, it is understood that theagitating members may have different thicknesses and/or transverselengths.

In the above described embodiment, the transverse length of theagitating member also at least in part defines the size (and at least inpart the direction) of the flow path along which the formulations andparticulates or other flowable components in the interior space of thechamber flows past the horn. For example, the horn may have a radius ofabout 0.875 inches (22.2 mm) and the transverse length of each ring is,as discussed above, about 0.5 inches (12.7 mm). The radius of the innersurface of the housing sidewall is approximately 1.75 inches (44.5 mm)so that the transverse spacing between each ring and the inner surfaceof the housing sidewall is about 0.375 inches (9.5 mm). It iscontemplated that the spacing between the horn outer surface and theinner surface of the chamber sidewall and/or between the agitatingmembers and the inner surface of the chamber sidewall may be greater orless than described above without departing from the scope of thisdisclosure.

In general, the horn 105 may be constructed of a metal having suitableacoustical and mechanical properties. Examples of suitable metals forconstruction of the horn 105 include, without limitation, aluminum,monel, titanium, stainless steel, and some alloy steels. It is alsocontemplated that all or part of the horn 105 may be coated with anothermetal such as silver, platinum, gold, palladium, lead dioxide, andcopper to mention a few. In one particularly suitable embodiment, theagitating members 137 are constructed of the same material as the horn105, and are more suitably formed integrally with the horn. In otherembodiments, one or more of the agitating members 137 may instead beformed separate from the horn 105 and connected thereto.

While the agitating members 137 (e.g., the rings) illustrated in FIG. 1are relatively flat, i.e., relatively rectangular in cross-section, itis understood that the rings may have a cross-section that is other thanrectangular without departing from the scope of this disclosure. Theterm “cross-section” is used in this instance to refer to across-section taken along one transverse direction (e.g., radially inthe illustrated embodiment) relative to the horn outer surface 107).Additionally, as seen of the first two and last two agitating members137 (e.g., the rings) illustrated in FIG. 1 are constructed only to havea transverse component, it is contemplated that one or more of theagitating members may have at least one longitudinal (e.g., axial)component to take advantage of transverse vibrational displacement ofthe horn (e.g., at the third agitating member as illustrated in FIG. 1)during ultrasonic vibration of the waveguide assembly 203.

As best illustrated in FIG. 1, the terminal end 113 of the waveguideassembly (e.g., of the horn 105 in the illustrated embodiment) issuitably spaced longitudinally from the inlet end 125 in FIG. 1 todefine what is referred to herein as a liquid intake zone in whichinitial swirling of liquid within the interior space 153 of the chamberhousing 151 occurs upstream of the horn 105. This intake zone isparticularly useful where the treatment chamber 151 is used for mixingtwo or more components together (such as with the particulates and theformulation or with two or more components of the formulation from inletend 125 in FIG. 1) whereby initial mixing is facilitated by the swirlingaction in the intake zone as the components to be mixed enter thechamber housing 151. It is understood, though, that the terminal end ofthe horn 105 may be nearer to the inlet end 125 than is illustrated inFIG. 1, and may be substantially adjacent to the inlet end 125 so as togenerally omit the intake zone, without departing from the scope of thisdisclosure.

Additionally, a baffle assembly, generally indicated at 245 is disposedwithin the interior space 153 of the chamber housing 151, and inparticular generally transversely adjacent the inner surface 167 of thesidewall 157 and in generally transversely opposed relationship with thehorn 105. In one suitable embodiment, the baffle assembly 245 comprisesone or more baffle members 247 disposed adjacent the inner surface 167of the housing sidewall 157 and extending at least in part transverselyinward from the inner surface of the sidewall 167 toward the horn 105.More suitably, the one or more baffle members 247 extend transverselyinward from the housing sidewall inner surface 167 to a positionlongitudinally intersticed with the agitating members 137 that extendoutward from the outer surface 107 of the horn 105. The term“longitudinally intersticed” is used herein to mean that a longitudinalline drawn parallel to the longitudinal axis of the horn 105 passesthrough both the agitating members 137 and the baffle members 247. Asone example, in the illustrated embodiment, the baffle assembly 245comprises four, generally annular baffle members 247 (i.e., extendingcontinuously about the horn 105) longitudinally intersticed with thefive agitating members 137.

As a more particular example, the four annular baffle members 247illustrated in FIG. 1 are of the same thickness as the agitating members137 in our previous dimensional example (i.e., 0.125 inches (3.2 mm))and are spaced longitudinally from each other (e.g., between opposedfaces of consecutive baffle members) equal to the longitudinal spacingbetween the rings (i.e., 0.875 inches (22.2 mm)). Each of the annularbaffle members 247 has a transverse length (e.g., inward of the innersurface 167 of the housing sidewall 157) of about 0.5 inches (12.7 mm)so that the innermost edges of the baffle members extend transverselyinward beyond the outermost edges of the agitating members 137 (e.g.,the rings). It is understood, however, that the baffle members 247 neednot extend transversely inward beyond the outermost edges of theagitating members 137 of the horn 105 to remain within the scope of thisdisclosure.

It will be appreciated that the baffle members 247 thus extend into theflow path of the formulations and particulates that flow within theinterior space 153 of the chamber 151 past the horn 105 (e.g., withinthe ultrasonic treatment zone). As such, the baffle members 247 inhibitthe formulations and particulates from flowing along the inner surface167 of the chamber sidewall 157 past the horn 105, and more suitably thebaffle members facilitate the flow of the formulations and particulatestransversely inward toward the horn for flowing over the agitatingmembers of the horn to thereby facilitate ultrasonic energization (i.e.,agitation) of the formulations and particulates to initiate mixing ofthe formulations and particulates within the carrier liquid to form themetal-modified particles. The baffle members further facilitate theprevention of agglomeration of the particles within the formulations.

In one embodiment, to inhibit gas bubbles against stagnating orotherwise building up along the inner surface 167 of the sidewall 157and across the face on the underside of each baffle member 247, e.g., asa result of agitation of the phases within the chamber, a series ofnotches (broadly openings) may be formed in the outer edge of each ofthe baffle members (not shown) to facilitate the flow of gas (e.g., gasbubbles) between the outer edges of the baffle members and the innersurface of the chamber sidewall. For example, in one particularlypreferred embodiment, four such notches are formed in the outer edge ofeach of the baffle members in equally spaced relationship with eachother. It is understood that openings may be formed in the bafflemembers other than at the outer edges where the baffle members abut thehousing, and remain within the scope of this disclosure. It is alsounderstood, that these notches may number more or less than four, asdiscussed above, and may even be completely omitted.

It is further contemplated that the baffle members 247 need not beannular or otherwise extend continuously about the horn 105. Forexample, the baffle members 247 may extend discontinuously about thehorn 105, such as in the form of spokes, bumps, segments or otherdiscrete structural formations that extend transversely inward fromadjacent the inner surface 167 of the housing sidewall 157. The term“continuously” in reference to the baffle members 247 extendingcontinuously about the horn does not exclude a baffle member as beingtwo or more arcuate segments arranged in end-to-end abuttingrelationship, i.e., as long as no significant gap is formed between suchsegments. Suitable baffle member configurations are disclosed in U.S.application Ser. No. 11/530,311 (filed Sep. 8, 2006), which is herebyincorporated by reference to the extent it is consistent herewith.

Also, while the baffle members 247 illustrated in FIG. 1 are eachgenerally flat, e.g., having a generally thin rectangular cross-section,it is contemplated that one or more of the baffle members may each beother than generally flat or rectangular in cross-section to furtherfacilitate the flow of bubbles along the interior space 153 of thechamber 151. The term “cross-section” is used in this instance to referto a cross-section taken along one transverse direction (e.g., radiallyin the illustrated embodiment, relative to the horn outer surface 107).

In one embodiment, as illustrated in FIG. 2, the treatment chamber mayfurther be in connection with a liquid recycle loop, generally indicatedat 400. Typically, the liquid recycle loop 400 is disposedlongitudinally between the inlet end 225 and the outlet port 265. Theliquid recycle loop 400 recycles a portion of the first and secondformulations being mixed within the interior space 253 of the housing251 back into the intake zone (generally indicated at 261) of theinterior space 253 of the housing 251. By recycling the first and secondformulations back into the intake zone, more effective mixing betweenthe formulations (and its components) and particulates can be achievedas the formulations and particulates are allowed to remain within thetreatment chamber, undergoing cavitation, for a longer residence time.Furthermore, the agitation in the upper portion of the chamber (i.e.,intake zone) can be enhanced, thereby facilitating better dispersingand/or dissolution of the particulates into the formulations.

The liquid recycle loop can be any system that is capable of recyclingthe liquid formulation from the interior space of the housing downstreamof the intake zone back into the intake zone of the interior space ofthe housing. In one particularly preferred embodiment, as shown in FIG.2, the liquid recycle loop 400 includes one or more pumps 402 to deliverthe formulation back into the intake zone 261 of the interior space 253of the housing 251. The liquid recycle loop 400 further includes a heatexchanger 404 to cool the formulation passing through the liquid recycleloop 400 prior to re-entering the intake zone 261 of the interior space253 of the housing 251.

Typically, the first and second formulations (and particulates) aredelivered back into the treatment chamber at a flow rate having a ratioof recycle flow rate to initial feed flow rate of the formulations(described below) of 1.0 or greater. While a ratio of recycle flow rateto initial feed flow rate is preferably greater than 1.0, it should beunderstood that ratios of less than 1.0 can be tolerated withoutdeparting from the scope of the present disclosure.

Although the energy created by the ultrasonic horn 233 substantiallyreduces agglomeration within the treatment chamber, many particulates,when initially added to a formulation, may still attract one another andclump together in large balls. Furthermore, many times, particles in theparticulate-containing formulations can settle out over time and attractone another to form large balls; referred to as reagglomeration. Assuch, in one embodiment, the ultrasonic mixing system may furthercomprise a filter assembly disposed at the outlet end of the treatmentchamber. The filter assembly can filter out the large balls ofparticulates that form within the particulate-containing formulationprior to the formulation being delivered to a packaging unit forconsumer use, as described more fully below. Specifically, the filterassembly is constructed to filter out particulates sized greater thanabout 0.2 microns.

Specifically, in one particularly preferred embodiment, the filterassembly covers the inner surface of the outlet port. The filterassembly includes a filter having a pore size of from about 0.5 micronto about 20 microns. More suitably, the filter assembly includes afilter having a pore size of from about 1 micron to about 5 microns, andeven more suitably, about 2 microns. The number and pour size of filtersfor use in the filter assembly will typically depend on the particulatesand formulation to be mixed within the treatment chamber.

A degasser may also be included in the ultrasonic mixing system. Forexample, once the prepared particulate-containing formulation exits thetreatment chamber, the particulate-containing formulation flows into adegasser in which excess gas bubbles are removed from theparticulate-containing formulation prior to the particulate-containingformulation being used into a consumer end-products.

One particularly preferred degasser is a continuous flow gas-liquidcyclone separator, such as commercially available from NATCO (Houston,Tex.). It should be understood by a skilled artisan, however, that anyother system that separates gas from an emulsion by centrifugal actioncan suitably be used without departing from the present disclosure.

In a third embodiment, the treatment chamber 351 has a general inlet end325 (a lower end in the orientation of the illustrated embodiment) and ageneral outlet end 327 (an upper end in the orientation of theillustrated embodiment). The treatment chamber 351 is configured suchthat the first and second formulations enter the treatment chamber 351generally at the inlet end 325 thereof, flow generally longitudinallywithin the chamber (e.g., upward in the orientation of illustratedembodiment) and exit the chamber generally at the outlet end 327 of thechamber. It should be recognized by one skilled in the art that thechamber of this particular embodiment may be oriented other than in avertical orientation and remain within the scope of this disclosure.

The inlet end 325 of the treatment chamber 351 is typically in fluidcommunication with at least one suitable delivery system that isoperable to direct a formulation to, and more suitably through, thechamber 151. More specifically, as illustrated in FIG. 3, two deliverysystems 328 and 329 are operable to direct a first formulation (notshown) and a second formulation (not shown) through the chamber 351.Typically, the delivery systems 328, 329 may independently comprise oneor more pumps 370 and 371, respectively, operable to pump the respectivephases from corresponding sources thereof to the inlet end 325 of thechamber 351 via suitable conduits 332, 334.

The treatment chamber 351 comprises a housing defining an interior space353 of the chamber 351 through which at least two formulations deliveredto the chamber 351 flow from the inlet end 325 to the outlet end 327thereof. The chamber housing 351 suitably comprises an elongate tube 355generally defining, at least in part, a sidewall 357 of the chamber 351.The tube 355 may have one or more inlet ports (two inlet ports aregenerally indicated in FIG. 3 at 356 and 358) formed therein throughwhich at least two separate formulations to be mixed within the chamber351 are delivered to the interior space 353 thereof. It should beunderstood by one skilled in the art that the inlet end of the housingmay include more than two inlet ports, more than three ports, and evenmore than four ports. By way of example, although not shown, the housingmay comprise three inlet ports, wherein the first inlet port and thesecond inlet port are suitably in parallel, spaced relationship witheach other, and the third inlet port is oriented on the oppositesidewall of the housing from the first and second inlet ports.

It should also be recognized by one skilled in the art that, whilepreferably the inlet ports are disposed in close proximity to oneanother in the inlet end, the inlet ports may be spaced farther alongthe sidewall of the chamber from one another without departing from thescope of the present disclosure.

As illustrated in FIG. 3, the treatment chamber may further be inconnection with a liquid recycle loop, generally indicated at 500.Typically, the liquid recycle loop 500 is disposed longitudinallybetween the inlet end 325 and the outlet end 327. The liquid recycleloop 500 recycles a portion of the first and second formulations beingmixed within the interior space 353 of the housing 351 back into anintake zone (generally indicated at 361) of the interior space 353 ofthe housing 351. By recycling the first and second formulations backinto the intake zone, more effective mixing between the formulations(and its components) and particulates can be achieved as theformulations and particulates are allowed to remain within the treatmentchamber, undergoing cavitation, for a longer residence time.Furthermore, the agitation in the upper portion of the chamber (i.e.,intake zone) can be enhanced, thereby facilitating better dispersingand/or dissolution of the particulates into the formulations.

The liquid recycle loop can be any system that is capable of recyclingthe liquid formulation from the interior space of the housing downstreamof the intake zone back into the intake zone of the interior space ofthe housing. In one particularly preferred embodiment, as shown in FIG.3, the liquid recycle loop 500 includes one or more pumps 502 to deliverthe formulation back into the intake zone 361 of the interior space 353of the housing 351. The liquid recycle loop 500 further includes a heatexchanger 504 to cool the formulation passing through the liquid recycleloop 500 prior to the formulation re-entering the intake zone 361 of theinterior space 353 of the housing 351.

Typically, the first and second formulations (and particulates) aredelivered back into the treatment chamber at a flow rate having a ratioof recycle flow rate to initial feed flow rate of the formulations(described below) of 1.0 or greater. While a ratio of recycle flow rateto initial feed flow rate is preferably greater than 1.0, it should beunderstood that ratios of less than 1.0 can be tolerated withoutdeparting from the scope of the present disclosure.

In operation according to one embodiment of the ultrasonic mixing systemof the present disclosure, the mixing system (more specifically, thetreatment chamber) is used to mix/disperse particulates into one or moreformulations. Specifically, a first formulation is delivered (e.g., bythe pumps described above) via conduits to the inlet end (FIGS. 1 and 2)or to one or more inlet ports formed in the treatment chamber housing(FIG. 3). The first formulation can be any suitable basic buffer systemknown in the art. For example, the first formulation may comprise sodiumbicarbonate, potassium hydroxide, sodium hydroxide, ammonium hydroxide,sodium carbonate, or combinations thereof.

Generally, from about 0.1 grams per minute to about 100,000 grams perminute of the first formulation is typically delivered into thetreatment chamber housing. More suitably, the amount of formulationdelivered into the treatment chamber housing is from about 1 gram perminute to about 10,000 grams per minute. In the preferred embodiment,the first formulation comprises aqueous sodium bicarbonate with aconcentration of from about 0.01 M to about 0.6 M. More preferably, thefirst formulation comprises aqueous sodium bicarbonate having aconcentration of 0.4 M.

With the ultrasonic horn turned on, the first formulation is pumpedthrough a conduit to the inlet end (FIGS. 1 and 2) or to an inlet portdisposed on the treatment chamber housing (FIG. 3). In one embodiment,as shown in FIGS. 1 and 2, the first formulation is pumped through theinlet end of the treatment chamber housing. The conduit through whichthe first formulation is delivered may be moved up and down duringdelivery to assure composition uniformity in the treatment chamber. Inanother embodiment, as shown in FIG. 3, the first formulation iscontinuously pumped through a conduit to an inlet port disposed at theinlet end 325 (a lower end in the orientation of the illustratedembodiment in FIG. 3) at a flow rate to maintain the requiredconcentration of the first formulation within the treatment chamber.

Additionally, the method includes delivering a second formulation, suchas those described above, to the interior space of the chamber. In oneembodiment, as shown in FIGS. 1 and 2, the second formulation is placedinto the interior of the chamber prior to the first formulation beingdelivered to the chamber. In another embodiment, the second formulationis continuously pumped through a conduit to an inlet port 358 disposedat the inlet end 325 (a lower end in the orientation of the illustratedembodiment in FIG. 3) at a flow rate to maintain the requiredconcentration of the first formulation within the treatment chamber. Inthis particular embodiment, the second formulation is delivered to thechamber at a rate of from about 0.0001 L/min to about 100 L/min.Preferably, the second formulation is delivered at a rate of from about0.001 L/min to about 0.100 L/min.

In accordance with the above embodiments, as the formulation andparticulates flow downward (as in FIGS. 1 and 2) or upward (as in FIG.3) within the chamber, the waveguide assembly, and more particularly thehorn assembly, is driven by the drive system to vibrate at apredetermined ultrasonic frequency. In response to ultrasonic excitationof the horn, the agitating members that extend outward from the outersurface of the horn dynamically flex/bend relative to the horn, ordisplace transversely (depending on the longitudinal position of theagitating member relative to the nodal region of the horn).

The formulations and particulates continuously flow longitudinally alongthe flow path between the horn assembly and the inner surface of thehousing sidewall so that the ultrasonic vibration and the dynamic motionof the agitating members cause cavitation in the formulation to furtherfacilitate agitation. The baffle members disrupt the longitudinal flowof formulation along the inner surface of the housing sidewall andrepeatedly direct the flow transversely inward to flow over thevibrating agitating members.

As the mixed particulate-containing formulation flows longitudinallypast the terminal end of the waveguide assembly, an initial back mixingof the particulate-containing formulation also occurs as a result of thedynamic motion of the agitating member at or adjacent the terminal endof the horn. Further, downstream flow of the particulate-containingformulation, as in FIGS. 1 and 2, results in the agitated formulationproviding a more uniform mixture of components (e.g., components offormulation and particulates) prior to exiting the treatment chamber viathe outlet port. Further, by utilizing ultrasonic energy created by theultrasonic horn described above, agglomeration of particles within thetreatment chamber is significantly reduced, and thus, a more fine andhomogenous powder may be produced upon isolation. In addition, it hasbeen found that by utilizing ultrasonic energy during the mixing of thefirst and second formulations described above, a metal-modified particlemay be formed that is capable of removing odorous compounds via chemicalabsorption.

In one embodiment, as illustrated in FIG. 2 and FIG. 3, as theparticulate-containing formulation travels through the chamber, aportion of the first and second formulations are directed out of thehousing prematurely through the liquid recycle loop as described above.This portion of the first and second formulations is then delivered backinto the intake zone of the interior space of the housing of thetreatment chamber to be mixed with fresh formulation and particulates.By recycling a portion of the first and second formulations, a morethorough mixing of the formulations and particulates occurs.

Once the particulate-containing formulation is thoroughly mixed, theparticulate-containing formulation exits the treatment chamber via theoutlet port. In one embodiment, once exited, the particulate-containingformulation can be directed to a post-processing delivery system to bedelivered to one or more packaging units where it may be used directlyfor spraying onto a material substrate or in a dip and squeeze process.

In another embodiment, the metal-modified particles may be recovered, orisolated, from the formulation by filtration and subsequently washed.For example, a fritted glass filter may be used where the pore size ofthe frit is smaller than the particulate size in diameter, length, orwidth, and this filter is attached to a filter flask. The particulatecontaining formulation is transferred to the filter, and a vacuum isapplied via a connection to the filter flask. The liquid component ofthe particulate containing formulation is pulled through the frittedfilter and separated from the particles. The particulates are washedwith water, and the same mechanism is used to isolate the particulatesfrom the wash liquid.

In a further embodiment, where isolated metal-modified particles aredesired for dry-condition applications, the aqueous solvent is removeden vacuo and the isolated particles are washed and dried. For example, arotovapor instrument, such as a Buchi Rotavapor R-114 from BuchiLabortechnik AG (Flawil, Switzerland), may be used to evaporate theliquid from the particulate containing formulation using applied heatand vacuum. The remaining particulate is collected and washed with waterusing a fritted filter attached to a flask. Further, theparticulate-containing formulation exiting the treatment chamber may bedirectly filtered to collect the isolated metal-modified particles andthen washed and air-dried.

The present disclosure is illustrated by the following examples whichare merely for the purpose of illustration and are not to be regarded aslimiting the scope of the disclosure or manner in which it may bepracticed.

Headspace Gas Chromatography for Quantitative Analysis of EthylMercaptan Removal

Quantitative analysis of odor adsorption was determined as described inthe Examples described below using Headspace Gas Chromatography. Theanalyses were conducted on an Agilent Technologies 5890, Series II gaschromatograph with an Agilent Technology 7694 headspace sampler obtainedfrom Agilent Technologies, Waldbronn, Germany. Helium was used as thecarrier gas with an injection port pressure of 12.7 psig, a headspacevial pressure of 15.8 psig, and a supply line pressure of 60 psig. ADB-624 column having a length of 30 meters and an internal diameter of0.25 millimeters was used for the odorous compound. Such a column isavailable from J&W Scientific, Inc. of Folsom, Calif. The operatingparameters used for the headspace gas chromatography are shown below inTable 1.

TABLE 1 Zone Temps, ° C. Oven 37 Loop 42 TR. Line 47 Event Time, minutesGC Cycle time 10.0 Vial eq. Time 10.0 Pressurized Time 0.20 Loop filltime 0.20 Loop eq. Time 0.15 Inject time 0.30 Vial Parameters First vial1 Last vial 1 Shake [off]

To test a sample, from about 3 mg to about 10 mg of the sample powderwas placed in a 20 cubic centimeter headspace vial. Using a syringe, analiquot of the odorous compound, methyl mercaptan, was transferred tothe side wall in the vial. The volume of ethyl mercaptan ranged fromabout 839 micrograms (about 1 microliter) to about 3356 micrograms(about 4 microliters). Each test sample was analyzed in triplicate.

After transfer of ethyl mercaptan to a test vial, the test vial wasimmediately sealed with a cap and a septum and placed in the headspacegas chromatography oven at 37° C. After a set equilibrium time ofapproximately 10 to 23 minutes, a hollow needle was inserted through theseptum and into the vial. A one cubic centimeter sample of theheadspace, or the air inside the vial, was then injected into the gaschromatograph.

Initially, a control vial with only the aliquot of ethyl mercaptan wastested to define 0% odorous compound adsorption. To calculate the amountof headspace odorous compound removed by each sample, the peak area forthe ethyl mercaptan from the vial with the sample was compared to thepeak area from the ethyl mercaptan control vial.

Example 1

In this Example, various types of silica particles were mixed withcopper chloride dihydrate dissolved in aqueous sodium bicarbonate withand without the presence of ultrasonic energy to form metal-modifiedsilica particles. The chemical mechanisms by which the metal-modifiedsilica particles remove odorous compounds were compared.

Three different samples were prepared using Snowtex®-OXS, Snowtex®-C,and Snowtex®-PSSO at 5% wt/wt in an aqueous suspension. Initially, a 100mL Snowtex®-OXS suspension was added to the ultrasonic chambercomprising the horn, agitating members, and baffle system describedabove in detail. 8.92 grams of copper chloride dihydrate was dissolvedin 700 mL of water, and this solution was added to the ultrasonicchamber. The ultrasonic mixing system was then ultrasonically activatedusing the ultrasonic drive system at 2.4 kW. 6.05 grams of sodiumbicarbonate was slowly added to the top of the ultrasonic mixing system.The mole ratio of copper (II) chloride dihydrate to the silica particleswas about 50:1, and the final concentration of sodium bicarbonate in thereaction suspension was about 0.04M.

This process was repeated for each of Snowtex®-C and Snowtex®-PSSO. Inthese two processes, however, the sodium bicarbonate was added to theultrasonic mixing system at the bottom of the chamber. Agglomeration andgelation were not observed for the processes utilizing Snowtex®-C andSnowtex®-PSSO. Agglomeration was observed, however, for the processutilizing Snowtex®-OXS.

Ethyl mercaptan (EtSH) removal assessment was carried out usingheadspace GC techniques, described in more detail below (See Example 4).Specifically, powder samples of CuOXS synthesized with and withoutultrasound energy by the methods described above were isolated viarotovap and washed with an excessive amount of water. Approximately 10mg of powder samples were placed in sample vials, followed by theinjection of 4 microliters of neat EtSH. The sample vials wereimmediately sealed and data collection commenced appropriately usingestablished protocols described above.

The data directed to the CuOXS preparation without the use of ultrasoundshowed increasing removal efficacy over time, which suggests a catalyticmechanism for removal of EtSH. The data directed to the CuOXSpreparation with the use of ultrasound, however, showed that the removalof EtSH by the ultrasonically prepared metal-modified silica particleswas stable over time. More specifically, this data suggests that therewas a finite chemical absorption over time, i.e., a saturation point mayhave been reached. As such, this data illustrates that chemicalabsorption is the odor removal mechanism for metal-modified silicaparticles prepared using ultrasonic energy. Chemical absorption ispreferred over catalysis, as chemical absorption involves the chemicalbinding of the odor compound to the odor removal compound, and thus, asopposed to catalysis, is irreversible when subject to physicalchallenges such as temperature and humidity. These results areillustrated in FIG. 4.

Example 2

In this Example, metal-modified silica particles were prepared withoutthe presence of ultrasonic energy. Specifically, a 5% wt/wt modifiedsilica suspension was prepared by mixing a 10% wt/wt silica suspension,a copper (II) chloride dihydrate solution, a sodium bicarbonatesolution, and water at the appropriate concentrations and volumes in abeaker. The mole ratio of copper (II) chloride dihydrate to silicaparticles was about 50:1, and the final concentration of sodiumbicarbonate in the reaction suspension was about 0.04 M. the volume ofthe reaction suspension was one liter. The silica suspension wasobtained from Nissan Chemical America Corporation of Houston, Tex. underthe tradename Snowtex® OXS, the copper (II) chloride dihydrate solutionwas obtained from Aldrich Chemical, and the sodium bicarbonate solutionwas obtained from Aldrich Chemical.

Specifically, the copper (II) chloride dihydrate solution was added tothe silica suspension as the silica suspension was vigorously stirredusing a magnetic stir bar. The sodium bicarbonate solution was thenslowly added at a rate of approximately 5 mL/min to the copper (II)chloride dihydrate solution and silica suspension. The final formulationcontained 5% wt/wt silica, a 50:1 ratio of copper ions to silicaparticles, and 0.04M (aq) sodium bicarbonate.

Isolation of solid copper modified silica particles was achieved byremoval of water en vacuo, followed by a wash with water and airfiltration. Specifically, a rotovapor instrument was used to evaporatethe liquid from the particulate containing formulation using appliedheat and vacuum. The remaining particulate was controlled and washedwith water using a fritted filter attached to a filter flask.

Example 3

This Example demonstrated the ability to form copper modified silicananoparticles using ultrasonic energy. Specifically, the process asdescribed above in Example 2 was carried out in an ultrasonic chamber ofan ultrasonic mixing system, as is described above in detail. Theultrasonic mixing system was ultrasonically activated using theultrasonic drive system at 2.4 kW prior to the addition of the sodiumbicarbonate solution. When the reaction temperature inside theultrasonic mixing system reached a temperature of 180° F., theultrasonic drive system was reduced to an output of 1.8 kW and remainedconstant through the remainder of the reaction. The particles were thenisolated in the same manner as described in Example 2.

Example 4

This Example demonstrated the effectiveness of copper modified silicananoparticles to remediate ethyl mercaptan. The modified silicaparticles of Example 2 and Example 3 were tested for ethyl mercaptanremediation using Headspace Gas Chromatography, as is described in moredetail below. In addition, activated carbon obtained from Meadwestvacoof Glenn Allen, Va. was tested for comparison. Measurement was recordedapproximately 25 minutes after introduction of ethyl mercaptan into asample vial containing either the modified silica particles of Example2, the modified silica particles of Example 3, or the activated carbon.The results are shown below in Table 2.

TABLE 2 mg ethyl mercaptan/ Sample g test sample CuOXS-no ultrasonic779.3 CuOXS-ultrasonic 300.3 Activated carbon 440.6

As shown in Table 2, the highest amount of ethyl mercaptan per gram oftest sample was removed by the CuOXS particles of Example 2, wherein noultrasonic energy was present. This data demonstrates that applicationof ultrasonic energy during the preparation of metal-modified silicaparticles does not interfere with the ability of the metal-modifiedsilica particles' ability to remediate ethyl mercaptan.

Example 5

This Example demonstrated the effectiveness of copper modified silicananoparticles to remediate ethyl mercaptan over a period of time. Themodified silica particles of Example 2 and Example 3 were tested forethyl mercaptan remediation using Headspace Gas Chromatography, as isdescribed in more detail below. In addition, activated carbon obtainedfrom Meadwestvaco of Glenn Allen, Va. was tested for comparison.Measurements were recorded over a 50 hour time period after introductionof ethyl mercaptan into a sample vial containing either the modifiedsilica particles of Example 2, the modified silica particles of Example3, or the activated carbon. The results are shown in FIG. 5.

From these results, it can be seen that the metal-modified silicaparticles remove odorous compounds via a catalytic mechanism when themodified particles are prepared without the presence of ultrasonicenergy, as the performance of these particles increases over time untilthe saturation point of the instrument is reached. The removal ofodorous compounds by metal-modified silica particles prepared in thepresence of ultrasonic energy, however, appears to level off beforereaching the detection limit. The plateau-effect of the particlesprepared in the presence of ultrasonic energy suggests that thesaturation of contact points for the odor compound to bind has beenreached.

Example 6

Distinct mechanisms by which copper modified silica particles preparedwith and without ultrasonic energy remediate ethyl mercaptan,respectively, were demonstrated. The modified silica particles ofExample 2 and Example 3 were tested for ethyl mercaptan remediation asdescribed using Headspace Gas Chromatography with variable temperatureover time. The GC oven was programmed from 30° C.-250° C. (held at 30°C. for 5 minutes, then ramped to 250° C. at 15° C./min, held at 250° C.for 4 minutes). In addition, activated carbon (obtained fromMeadwestvaco of Glenn Allen, Va.) was tested for comparison purpose.Measurement was recorded approximately 3 hours after introduction ofethyl mercaptan into the sample vial. The results are shown in FIG. 6 interms of peak area (arbitrary units) and retention time. The peak atapproximately 3.5 minutes represents EtSH, while the peak atapproximately 13.5 minutes represents the disulfide derivative (EtSSEt)of EtSH.

Example 7

Identification of the disulfide derivative conversion product by themodified silica particles from Example 2 was demonstrated. The modifiedsilica particles from Example 2 and Example 3 assessed for ethylmercaptan remediation using headspace gas chromatography coupled withmass spectroscopy. An Agilent Technologies 5973N GC/MS with a 6890 gaschromatograph was used to analyze the samples. The samples were analyzedon a J&W DB-5MS capillary column (60 m×0.25 mm×0.25 u film) using splitinjection (100:1 split at 225° C.). The GC oven was programmed from 50°C. (held for 2 minutes) to 300° C. at 25° C./min. Mass spectra wereacquired with ionization energy of 70 eV scanning from 35-250 Da at 3.39spectra/second. Data was collected and analyzed with ChemStationsoftware supplied with the instrument. The 20 ml headspace vials weresealed with PTFE/Silicone/PTFE septa, and the gas samples collected witha 25 μl Valco Precision Series A-2 sampling syringe. The results areshown in FIGS. 7A and 7B in terms of mass-to charge ratio (M/Z). Themass spectrum (A) corresponds to the GC peak at approximately 3.5minutes (r.t.) and exhibits an M/Z 62, which is identified as ethylmercaptan. The mass spectrum (B) corresponds to the GC peak atapproximately 13.5 minutes (r.t.) and exhibits an M/Z 122, which isidentified as diethyl disulfide.

Example 8

Identification of two distinct copper species on copper-modified silicaparticles from Example 2 and Example 3, respectively, was demonstrated.Electron paramagnetic resonance (EPR) spectroscopy was used to identifythe nature of the copper species on copper-modified silica particlesfrom Example 2 and Example 3. The EPR spectrum A in FIG. 8A correspondsto copper-modified silica particles from Example 2; the asymmetricspectrum suggests the presence of both isolated and clustered copperspecies. The EPR spectrum B in FIG. 8B corresponds to copper-modifiedsilica particles from Example 3; the relatively symmetric spectrumsuggests the presence of predominantly isolated copper species.

Example 9

The copper content in copper-modified silica particles in Example 2 andExample 3, respectively, was determined using inductively coupled plasma(ICP) spectrometry. The results are shown in Table 3.

TABLE 3 Copper content Description (%) Copper-modified silica particles,2.78 Example 2-a Copper-modified silica particles, 2.74 Example 2-bCopper-modified silica particles, 2.53 Example 2-c Copper-modifiedsilica particles, 2.67 Example 3-a Copper-modified silica particles,2.61 Example 3-b Copper-modified silica particles, 2.56 Example 3-c

Example 10

X-ray photoelectron spectroscopy (XPS) was performed on copper modifiedsilica particles from Example 2 (CuOXS-2) and copper modified silicaparticles from Example 3 (CuOXS-3) for identifying the chemical natureof copper species. XPS spectra are presented in FIG. 9A and FIG. 9B.Each spectrum was shifted to match the adventitious carbon peak (284.8eV). In both the samples important elements were analyzed for theirchemical origin and are tabulated in Table 4.

TABLE 4 Sample CuOXS-1 CuOXS-2 Chemical Chemical Element Peak originPeak Origin C 284.80 C═O 284.80 C—OH 287.41 286.67 C═O 287.30 O 532.88C—O 532.65 C—O 535.33 C═O 535.77 C═O Si 103.41 SiO₂ 99.04 Si 105.99 Ga99.75 Si 98.93 Si 103.26 SiO₂ 106.43 Ga Cu 935.61 CuCl2 Cu No copper936.45 not identified peaks were 937.96 not identified observed 942.81not identified 944.85 not identified 946.69 not identified

XPS spectra of CuOXS-1 sample shows several peaks related to coppercompounds. However, only one peak could be identified and is related toCuCl2 (from NIST database). CuOXS-2 sample spectra do not have peaksrelated to copper. The absence of Cu peak in the XPS spectra could bedue to some coating on the particles surface. Since XPS probes only fewatomic surface layers, copper species coated with some organic/inorganiclayer will be difficult to identify using this technique.

Example 11

BJH pore size analyses for copper modified silica particles from Example2 (CuOXS50 1) and copper modified silica particles from Example 3(CuOXS50 2) showed higher pore volumes for CuOXS50 2. Results are shownin FIG. 10. The area under each curve represents the pore volume for therespective sample.

The data from Examples 6-11 strongly demonstrates the compositionaldifferentiation of copper modified silica particles from Example 2 andExample 3 and how each, respectively, remediates ethyl mercaptandifferently. Example 6 and Example 7 are gas chromatography-headspaceand gas chromatography-headspace coupled with mass spectrometryexperiments. The data shows the conversion of ethyl mercaptan to itsdisulfide derivative diethyl disulfide by copper modified silicaparticles from Example 2. This reaction mechanism is, therefore,catalytic in nature; and those skilled in the art should be able torecognize the reaction mechanism applies to odorous compounds withsimilar redox potential. Examples of such compounds include organiccompounds with aldehyde and acid functional groups. For copper modifiedsilica particles from Example 3, the data shows a chemical absorptionmechanism with evidence of auto-oxidation of a low concentration ofethyl mercaptan to its disulfide derivative. Those skilled in the artshould recognize the tendency of sulfide containing compounds toauto-oxidate under ambient conditions. Additionally, data from Example 6demonstrates evidence of such auto-oxidation in test samples notcontaining copper modified silica particles.

Data from Example 8 demonstrates the unique difference in the copperspecies in copper modified silica particles from Example 2 and Example3, respectively. The electron paramagnetic spectroscopic (EPR) spectrumfor copper modified silica particles from Example 2 is asymmetric, whichsuggests the nature of the copper species is clustered. The EPR spectrumfor copper modified silica particles from Example 3 is more symmetric,which suggests the presence of dominantly isolated copper species. Thoseskilled in the art should recognize the difference in EPR spectrastrongly suggests two unique and different copper species in coppermodified silica particles from Example 2 and Example 3.

Example 9 demonstrates the presence of copper in copper modified silicaparticles from Example 2 and Example 3 at comparable concentration. Datafrom Example 10 demonstrates that, despite the presence of copper (datafrom Example 9), the orientation and positioning of copper species onthe silica surface in copper modified silica particles from Example 2and Example 3 are distinct and different.

In Example 10, the nature of the characterization technique analyzes forcopper at the top 100 nanometer layer of the material. No presence ofcopper was detected for copper modified silica particles from Example 3,while copper was detected for copper modified silica particles fromExample 2. This difference, combined with data from Example 9demonstrating the comparable presence of copper in copper modifiedsilica particles from Example 2 and Example 3, strongly suggests thecopper species are different, respectively.

Data in Example 11 demonstrates a higher concentration of pore volume incopper modified silica particles from Example 3 compared to Example 2.This data suggests the trigger for the unique composition in coppermodified silica particles from Example 3 may be due to a cavitationmechanism enabled by use of ultrasonic energy. The cavitation, thereby,allows for copper to be deposited onto the silica surface in a mannerthat favors isolated copper species; consequently, this uniquecomposition of copper modified silica particles remediate ethylmercaptan differently than copper modified silica particles from Example2.

When introducing elements of the present disclosure or preferredembodiments thereof, the articles “a”, “an”, “the”, and “said” areintended to mean that there are one or more of the elements. The terms“comprising”, “including”, and “having” are intended to be inclusive andmean that there may be additional elements other than the listedelements.

As various changes could be made in the above constructions and methodswithout departing from the scope of the invention, it is intended thatall matter contained in the above description and shown in theaccompanying drawings shall be interpreted as illustrative and not in alimiting sense.

1. A composition comprising particles with a transition metal imbeddedtherein, wherein the mole ratio of transition metal to particles is fromabout 25:1 to about 50:1, wherein the composition is prepared in thepresence of ultrasonic energy, and wherein the particles are selectedfrom the group consisting of organic particles, inorganic particles, andmetal particles.
 2. The composition of claim 1, wherein the particlesare inorganic particles selected from the group consisting of silicaparticles and alumina particles.
 3. The composition of claim 2, whereinthe particles are silica particles.
 4. The composition of claim 1,wherein the transition metal is selected from the group consisting ofscandium, titanium, vanadium, chromium, manganese, iron, cobalt, nickel,copper, zinc, silver, and gold.
 5. The composition of claim 1, whereinthe transition metal is copper.
 6. The composition of claim 1, whereinthe particles with the transition metal imbedded therein are forremoving an odorous compound from a liquid or gas by chemicaladsorption.
 7. A composition comprising particles with a transitionmetal imbedded therein, wherein the particles are selected from thegroup consisting of organic particles, inorganic particles, and metalparticles, and wherein the composition is prepared by a processcomprising: providing a treatment chamber comprising an interior spaceand an elongate ultrasonic waveguide assembly positioned within theinterior space; delivering a first formulation into the interior spaceof the chamber; delivering a second formulation separately from thefirst formulation into the interior space of the chamber; ultrasonicallymixing the first and second formulations via the elongate ultrasonicwaveguide assembly operating in a predetermined ultrasonic frequency. 8.The composition as set forth in claim 7, wherein the first formulationcomprises a basic buffer system.
 9. The composition as set forth inclaim 8, wherein the basic buffer system is selected from the groupconsisting of aqueous sodium bicarbonate, potassium hydroxide, sodiumhydroxide, ammonium hydroxide, sodium carbonate, and combinationsthereof.
 10. The composition as set forth in claim 8, wherein the firstformulation is delivered into the interior space of the chamber at arate of from about 0.1 grams per minute to about 100,000 grams perminute.
 11. The composition as set forth in claim 7, wherein the secondformulation comprises a salt of a transition metal and particles,wherein the particles are selected from the group consisting of organicparticles, inorganic particles, and metal particles.
 12. The compositionas set forth in claim 11, wherein the second formulation is delivered tothe interior space of the chamber such that the particles of the secondformulation are present in an amount of at least about 4% (by weight ofthe second formulation).
 13. The composition as set forth in claim 11,wherein the second formulation is delivered to the interior space of thechamber at a rate of from about 0.0001 L/min to about 100 L/min.
 14. Thecomposition as set forth in claim 11, wherein the transition metal isselected from the group consisting of scandium, titanium, vanadium,chromium, manganese, iron, cobalt, nickel, copper, zinc, silver, andgold.
 15. The composition of claim 11, wherein the transition metal iscopper.
 16. The composition of claim 7, wherein the particles with thetransition metal imbedded therein are for removing an odorous compoundfrom a liquid or gas by chemical adsorption.
 17. The composition ofclaim 1, wherein the mole ratio of transition metal to particles isabout 50:1.